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1. 发明申请

WO2010019770A2 CONTROL SYSTEM FOR A WORK UNIT 审中-公开
标题翻译：工作单位控制系统
公开(公告)号：WO2010019770A2
公开(公告)日：2010-02-18
申请号：PCT/US2009053712
申请日：2009-08-13
申请人： VERMEER MFG CO , MASS CORY , GRAHAM CURT , HUTCHINSON MATTHEW
发明人： MASS CORY , GRAHAM CURT , HUTCHINSON MATTHEW
IPC分类号： A01B69/00 , A01B76/00 , B62D11/02 , B62D11/20
CPC分类号： B62D1/12 , A01B33/028 , A01B69/007 , B62D11/006 , B62D11/04 , B62D51/001 , B62D51/04
摘要： The present disclosure relates to a work unit with power turning. The work unit includes a frame having a first end, a second end and left and right sides that extend between the first and second ends. A work element is carried by the frame. A left propulsion element is positioned at the left side of the frame and a right propulsion element is positioned at the right side of the frame. A drive arrangement is carried by the frame for driving the left and right propulsion elements. The work unit also includes left and right spaced-apart leverage arms that project outwards from the second end of the frame. At least one of the left and right leverage arms is operatively connected to the drive arrangement such that pressure applied by an operator to the left or right leverage arms in a left or right direction causes the drive arrangement to turn the work unit.
摘要翻译：本公开涉及具有动力转向的作业单元。工作单元包括具有在第一端和第二端之间延伸的第一端，第二端以及左右两侧的框架。工件由框架承载。左推进元件位于框架的左侧，右推进元件位于框架的右侧。驱动装置由用于驱动左右推进元件的框架承载。工作单元还包括从框架的第二端向外突出的左和右间隔开的杠杆臂。左和右杠杆臂中的至少一个可操作地连接到驱动装置，使得操作者向左或右杠杆臂施加的压力在左或右方向上使杠杆臂驱动装置转动。

2. 发明申请

WO2008027381A3 HYDROCARBON BASED SULFUR SOLVENT SYSTEMS AND METHODS 审中-公开
公开(公告)号：WO2008027381A3
公开(公告)日：2008-03-06
申请号：PCT/US2007/018919
申请日：2007-08-28
申请人： FLUOR TECHNOLOGIES CORPORATION , GRAHAM, Curt , HENDERSON, Robert , NIELSEN, Richard B. , DEBEST, Michael
发明人： GRAHAM, Curt , HENDERSON, Robert , NIELSEN, Richard B. , DEBEST, Michael
IPC分类号： C10G17/00 , C10G45/00
摘要： Contemplated configurations and methods for elemental sulfur removal from various gases, and especially well acid gases employ a hydrocarbon solvent that dissolves the sulfur to form a rich solvent and that is then regenerated by hydrotreating. Thus, sulfur is removed from the rich solvent as H2S that may then be processed (e.g., in Claus unit or absorption unit) while the regenerated solvent is routed back to the well and associated production pipes.

3. 发明申请

WO2006004723A1 LNG REGASIFICATION CONFIGURATIONS AND METHODS 审中-公开
标题翻译： LNG重组配置和方法
公开(公告)号：WO2006004723A1
公开(公告)日：2006-01-12
申请号：PCT/US2005/022880
申请日：2005-06-27
申请人： FLUOR TECHNOLOGIES CORPORATION , MAK, John , NEUMANN, Ralph , GRAHAM, Curt , HEFFERN, Dan
发明人： MAK, John , NEUMANN, Ralph , GRAHAM, Curt , HEFFERN, Dan
IPC分类号： F25J3/00
CPC分类号： F25J3/0214 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/04 , F25J2200/72 , F25J2200/74 , F25J2205/04 , F25J2215/62 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/02 , F25J2290/10
摘要： LNG composition of LNG from a storage tank or other source is modified in a process in which the LNG is pumped to a first pressure and split into two portions. One portion of the pressurized LNG is then reduced in pressure and heavier components are separated from the reduced pressure LNG to thereby form a lean LNG. The lean LNG is then pumped to a higher pressure and combined with the other portion to form a leaner LNG. Preferably, separation is performed using a demethanizer, wherein part of the demethanizer overhead product is condensed to form the lean LNG, while another portion is used for column reflux. In further preferred configurations, ethane recovery is variable and in yet other configurations, propane or ethane can be delivered via a batching pipeline.
摘要翻译：来自储罐或其他来源的LNG的LNG组成在LNG被泵送到第一压力并分成两部分的过程中被修改。然后将一部分加压LNG压力降低，并将较重组分从减压LNG中分离出来，从而形成贫LNG。然后将贫LNG泵送到更高的压力并与另一部分结合以形成更贫乏的LNG。优选地，使用脱甲烷塔进行分离，其中部分脱甲烷塔塔顶产物被冷凝以形成贫LNG，而另一部分被用于塔回流。在进一步优选的构造中，乙烷回收是可变的，并且在其他构造中，丙烷或乙烷可以通过配料管道输送。

4. 发明申请

WO2008027381A2 HYDROCARBON BASED SULFUR SOLVENT SYSTEMS AND METHODS 审中-公开
标题翻译：基于石油的硫化物溶剂系统和方法
公开(公告)号：WO2008027381A2
公开(公告)日：2008-03-06
申请号：PCT/US2007018919
申请日：2007-08-28
申请人： FLUOR TECH CORP , GRAHAM CURT , HENDERSON ROBERT , NIELSEN RICHARD B , DEBEST MICHAEL
发明人： GRAHAM CURT , HENDERSON ROBERT , NIELSEN RICHARD B , DEBEST MICHAEL
IPC分类号： C10G49/22
CPC分类号： B01D53/1456 , B01D53/047 , B01D2257/304 , B01D2257/306 , C01B17/033 , C01B17/0404 , C01B17/162 , C10L3/10 , C10L3/102
摘要： Contemplated configurations and methods for elemental sulfur removal from various gases, and especially well acid gases employ a hydrocarbon solvent that dissolves the sulfur to form a rich solvent and that is then regenerated by hydrotreating. Thus, sulfur is removed from the rich solvent as H2S that may then be processed (e.g., in Claus unit or absorption unit) while the regenerated solvent is routed back to the well and associated production pipes.
摘要翻译：用于从各种气体，特别是良好酸性气体中元素除去硫的考虑的构造和方法使用溶解硫以形成富溶剂的烃溶剂，然后通过加氢处理再生。因此，将硫从富溶剂中除去，然后可以将H 2 S作为H2S进行处理（例如，在克劳斯单元或吸收单元中），同时将再生溶剂返回到井和相关联的生产管道。

5. 发明申请

WO2007030243A1 APPARATUS FOR CONTROL OF A MOBILE MACHINE 审中-公开
标题翻译：控制移动机器的设备
公开(公告)号：WO2007030243A1
公开(公告)日：2007-03-15
申请号：PCT/US2006/030448
申请日：2006-08-03
申请人： VERMEER MANUFACTURING COMPANY , GRAHAM, Curt , SHKIRYAK, Peter , HUTCHINSON, Matthew
发明人： GRAHAM, Curt , SHKIRYAK, Peter , HUTCHINSON, Matthew
IPC分类号： E02F9/20 , G05G9/047
CPC分类号： G05G9/047 , E02F9/2004
摘要： A control system(50) for use with a mobile machine (100) . The control system including a hand-grip bar (140) having right (146) and left (142) curved sections. The curved sections each define an approximate center (c) . The control system further including joysticks (122, 124) positioned at the approximate center of the curved sections . The curved sections each have a radius such that an operator can operate one or both joysticks without releasing his grip from the hand-grip bar.
摘要翻译：一种与移动机器（100）一起使用的控制系统（50）。该控制系统包括具有右（146）和左（142）弯曲部分的手柄杆（140）。弯曲部分每个限定近似中心（c）。控制系统还包括位于弯曲部分的大致中心处的操纵杆（122,124）。弯曲部分各自具有半径，使得操作者可以操作一个或两个操纵杆，而不会将其从手柄杆释放。

6. 发明申请

WO2005045337A1 LNG VAPOR HANDLING CONFIGURATIONS AND METHODS 审中-公开
标题翻译： LNG蒸汽处理配置和方法
公开(公告)号：WO2005045337A1
公开(公告)日：2005-05-19
申请号：PCT/US2004/019490
申请日：2004-06-17
申请人： FLUOR CORPORATION , MAK, John , NIELSEN, Richard, B. , GRAHAM, Curt
发明人： MAK, John , NIELSEN, Richard, B. , GRAHAM, Curt
IPC分类号： F25J1/00
CPC分类号： F17C9/00 , F17C3/00 , F17C5/06 , F17C6/00 , F17C9/04 , F17C2201/052 , F17C2205/0364 , F17C2205/0367 , F17C2221/033 , F17C2221/035 , F17C2223/0161 , F17C2223/033 , F17C2223/043 , F17C2223/047 , F17C2225/0123 , F17C2225/0153 , F17C2225/0161 , F17C2225/033 , F17C2225/035 , F17C2225/036 , F17C2225/047 , F17C2227/0128 , F17C2227/0135 , F17C2227/0157 , F17C2227/0178 , F17C2227/0185 , F17C2227/0306 , F17C2227/0309 , F17C2227/0318 , F17C2227/0327 , F17C2227/0339 , F17C2227/0388 , F17C2227/0393 , F17C2250/0636 , F17C2250/0642 , F17C2260/02 , F17C2260/031 , F17C2260/056 , F17C2265/015 , F17C2265/022 , F17C2265/025 , F17C2265/03 , F17C2265/033 , F17C2265/034 , F17C2265/036 , F17C2265/037 , F17C2265/05 , F17C2270/0105 , F17C2270/0123 , F17C2270/0136 , F25J3/0214 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2205/90 , F25J2210/04 , F25J2210/62 , F25J2210/90 , F25J2235/60 , F25J2245/02 , F25J2245/90 , F25J2270/904 , F25J2290/62
摘要： LNG vapor from an LNG storage vessel is absorbed using C 3 and heavier components provided by a fractionator that receives a mixture of LNG vapors and the C 3 and heavier components as fractionator feed. In such configurations, refrigeration content of the LNG liquid from the LNG storage vessel is advantageously used to condense the LNG vapor after separation. Where desired, a portion of the LNG liquid may also be used as fractionator feed to produce LPG as a bottom product.
摘要翻译：来自LNG储存容器的LNG蒸汽被C3和较重的组分吸收，分配器由接收LNG蒸汽和C3和较重组分的混合物的分馏器提供，作为分馏塔进料。在这种结构中，来自LNG储存容器的LNG液体的制冷含量有利地用于在分离后冷凝LNG蒸气。在需要的情况下，一部分LNG液体也可以用作分馏塔进料以产生作为底部产物的LPG。

7. 发明申请

WO2003089115A1 CONFIGURATIONS AND METHODS FOR IMPROVED ACID GAS REMOVAL 审中-公开
标题翻译：改善酸性气体去除的配置和方法
公开(公告)号：WO2003089115A1
公开(公告)日：2003-10-30
申请号：PCT/US2002/012050
申请日：2002-04-15
申请人： FLUOR CORPORATION , MAK, John , GRAHAM, Curt , NIELSEN, Richard
发明人： MAK, John , GRAHAM, Curt , NIELSEN, Richard
IPC分类号： B01D53/14
CPC分类号： B01D53/1493 , B01D53/1475 , Y02C10/06
摘要： A plant includes an absorber (103) that operates in a gas phase supercritical region and removes an acid gas from a feed stream (9) at high recovery of the feed stream (10) while producing a high purity acid gas stream (36). Particularly preferred plants include gas purification plants that receive a feed gas with at least 5 mol % carbon dioxide at a pressure of at least 3000 psi.
摘要翻译：植物包括在气相超临界区域中操作并在高回收率的进料流（10）中从进料流（9）中除去酸性气体同时产生高纯酸性气流（36）的吸收器（103）。特别优选的设备包括气体净化设备，其在至少3000psi的压力下接收具有至少5mol％二氧化碳的进料气体。

8. 发明申请

WO2008027381B1 HYDROCARBON BASED SULFUR SOLVENT SYSTEMS AND METHODS 审中-公开
公开(公告)号：WO2008027381B1
公开(公告)日：2008-06-12
申请号：PCT/US2007018919
申请日：2007-08-28
申请人： FLUOR TECH CORP , GRAHAM CURT , HENDERSON ROBERT , NIELSEN RICHARD B , DEBEST MICHAEL
发明人： GRAHAM CURT , HENDERSON ROBERT , NIELSEN RICHARD B , DEBEST MICHAEL
IPC分类号： C10G17/00 , C10G45/00
CPC分类号： B01D53/1456 , B01D53/047 , B01D2257/304 , B01D2257/306 , C01B17/033 , C01B17/0404 , C01B17/162 , C10L3/10 , C10L3/102
摘要： Contemplated configurations and methods for elemental sulfur removal from various gases, and especially well acid gases employ a hydrocarbon solvent that dissolves the sulfur to form a rich solvent and that is then regenerated by hydrotreating. Thus, sulfur is removed from the rich solvent as H2S that may then be processed (e.g., in Claus unit or absorption unit) while the regenerated solvent is routed back to the well and associated production pipes.

9. 发明申请

WO2007014069A2 NGL RECOVERY METHODS AND CONFIGURATIONS 审中-公开
标题翻译： NGL恢复方法和配置
公开(公告)号：WO2007014069A2
公开(公告)日：2007-02-01
申请号：PCT/US2006028471
申请日：2006-07-20
申请人： FLUOR TECH CORP , MAK JOHN , NIELSEN RICHARD B , GRAHAM CURT
发明人： MAK JOHN , NIELSEN RICHARD B , GRAHAM CURT
IPC分类号： F25J3/00
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2210/06 , F25J2215/60 , F25J2220/66 , F25J2240/02 , F25J2240/40 , F25J2245/02 , F25J2280/02
摘要： Contemplated NGL plants include a feed gas bypass circuit through which a portion of the feed gas is provided downstream to a vapor portion of the feed gas to thereby increase turbo expander inlet temperature and demethanizer temperature. Contemplated configurations are especially advantageous for feed gases with relatively high carbon dioxide content as they entirely avoid carbon dioxide freezing in the demethanizer, provide additional power production by the turboexpander, and recover C2+ components to levels of at least 80% while achieving a low carbon dioxide content in the NGL product.
摘要翻译：考虑的NGL装置包括原料气旁通回路，通过该原料气一部分原料气被提供到原料气的蒸气部分的下游，从而增加涡轮膨胀机入口温度和脱甲烷塔温度。考虑到的构造对于二氧化碳含量相对较高的原料气特别有利，因为它们完全避免了脱甲烷器中的二氧化碳冻结，通过涡轮膨胀机提供额外的动力产生，并且将C2 +组分回收至至少80％的水平，同时实现低二氧化碳内容在NGL产品中。

10. 发明申请

WO2006066015A2 CONFIGURATIONS AND METHODS FOR LNG REGASIFICATION AND BTU CONTROL 审中-公开
标题翻译： LNG注册和BTU控制的配置和方法
公开(公告)号：WO2006066015A2
公开(公告)日：2006-06-22
申请号：PCT/US2005045455
申请日：2005-12-13
申请人： FLUOR TECH CORP , MAK JOHN , GRAHAM CURT
发明人： MAK JOHN , GRAHAM CURT
IPC分类号： B01D1/14
CPC分类号： F17C9/02 , F17C5/06 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2225/0115 , F17C2225/0123 , F17C2225/035 , F17C2227/0135 , F17C2227/0185 , F17C2227/0309 , F17C2227/0318 , F17C2227/0332 , F17C2227/0393 , F17C2227/0395 , F17C2260/056 , F17C2265/015 , F17C2265/05 , F17C2270/0105 , F17C2270/0121 , F17C2270/0123 , F17C2270/0136 , F25J3/0209 , F25J3/0214 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/04 , F25J2200/70 , F25J2200/74 , F25J2200/78 , F25J2205/04 , F25J2215/62 , F25J2230/08 , F25J2230/60 , F25J2240/02 , F25J2245/02
摘要： LNG is pumped to supercritical pressure and vaporized, preferably in an offshore location to thereby form a natural gas stream with an intermediate temperature. A first portion of that stream is then processed in an onshore location to remove at least some non-methane components to thereby form a lean LNG, which is then combined with a second portion of that stream to form a sales gas having desired chemical composition. The intermediate temperature and the split ratio of the gas stream in first and second portion are a function of the concentration of the non-methane components in the LNG.
摘要翻译： LNG被泵送到超临界压力并蒸发，优选在海上位置，从而形成具有中间温度的天然气流。然后将该物流的第一部分在陆上处理以除去至少一些非甲烷组分，从而形成贫LNG，然后将其与该流的第二部分组合以形成具有所需化学成分的销售气体。第一和第二部分中的气流的中间温度和分流比是LNG中非甲烷组分的浓度的函数。

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